Steam reformer with recuperative heat exchanger
View Patent ↗Embodiments are disclosed that relate to temperature distribution in a reaction chamber of a steam reformer. For example, one disclosed embodiment provides a steam reformer, comprising a central chamber through which feed gas flows, a reaction chamber surrounding the central chamber and having an inner wall and an outer wall, and a recuperative heat exchanger disposed between the inner wall of the reaction chamber and the central chamber.
1. A steam reformer, comprising:
a central chamber through which feed gas flows;
a water-gas shift reaction chamber, configured to generate a reformate via a water-gas shift reaction, surrounding the central chamber and having a first inner wall and a first outer wall; and
a recuperative heat exchanger extending from above a top portion of the reaction chamber past a bottom portion of the reaction chamber and disposed interior to the reaction chamber and having a second outer wall, the first inner wall and second outer wall forming a shared wall.
2. The steam reformer of claim 1 , wherein the central chamber, the heat exchanger, and the reaction chamber are concentric about a longitudinal axis of the steam reformer.
3. The steam reformer of claim 1 , wherein the heat exchanger and the reaction chamber are adjacent.
4. The steam reformer of claim 1 , wherein the heat exchanger and the central chamber are adjacent, and a second inner wall of the heat exchanger and a wall of the central chamber form a shared wall.
5. The steam reformer of claim 1 , further comprising a feed gas inlet at a bottom of the central chamber and a feed gas outlet at a top of the central chamber, the central chamber having a first flow direction.
6. The steam reformer of claim 1 , further comprising a feed gas inlet at a top of the heat exchanger and a feed gas outlet at a bottom of the heat exchanger, the heat exchanger having a second flow direction.
7. The steam reformer of claim 1 , further comprising a feed gas inlet at a bottom of the reaction chamber and a reformate outlet at a top of the reaction chamber, the reaction chamber having a first flow direction.
8. The steam reformer of claim 1 , further comprising an expansion region disposed at an outlet of the heat exchanger.
9. The steam reformer of claim 8 , wherein, at the expansion region, the second outer wall of the heat exchanger curves inward toward a second inner wall of the heat exchanger with a first radius of curvature and stops at a first position.
10. The steam reformer of claim 9 , wherein, at the expansion region, the second inner wall of the heat exchanger curves inward with a second radius of curvature which is greater than the first radius of curvature to a second position and then curves downward and extends parallel to a longitudinal axis of the steam reformer to a bottom of the steam reformer.
11. The steam reformer of claim 1 , wherein the heat exchanger has a width of 1.5 mm.
12. A steam reformer, comprising:
a central chamber through which feed gas flows;
a water-gas shift reaction chamber comprising a catalyst, configured to generate a reformate via a water-gas shift reaction, surrounding the central chamber and having an inner wall and an outer wall;
a recuperative heat exchanger extending from above a top portion of the reaction chamber past a bottom portion of the reaction chamber and disposed between the inner wall of the reaction chamber and the central chamber; and
an expansion region disposed at an outlet of the recuperative heat exchanger and configured to create a uniform distribution of gas at an inlet of the reaction chamber.
13. The steam reformer of claim 12 , wherein the central chamber and the heat exchanger are adjacent and the reaction chamber and the heat exchanger are adjacent, and wherein the central chamber, the heat exchanger, and the reaction chamber are concentric about a longitudinal axis of the steam reformer.
14. The steam reformer of claim 12 , wherein a thickness of the heat exchanger increases at the expansion region.
15. The steam reformer of claim 12 , wherein the feed gas flows through the central chamber in a first direction, through the heat exchanger in a second direction which is opposite to the first direction, and through the reaction chamber in the first direction, and wherein the central chamber, the heat exchanger, and the reaction chamber form a continuous flow path.
16. The steam reformer of claim 12 , wherein a reformate is generated in the reaction chamber, and the reformate is routed to a fuel cell stack coupled to the steam reformer via a first pipe.
17. The steam reformer of claim 16 , wherein the fuel cell stack is coupled to a building heating system.
18. A system, comprising:
a fuel cell stack;
a main reformer operable to generate a feed gas; and
an auxiliary reformer operable to generate a reformate fuel for the fuel cell stack, comprising:
a cylindrical central chamber through which the feed gas from the main reformer flows;
an annular reaction chamber, configured to generate a reformate via a water-gas shift reaction, surrounding the central chamber and having an inner wall and an outer wall;
an annular recuperative heat exchanger extending from above a top portion of the reaction chamber past a bottom portion of the reaction chamber and disposed between the inner wall of the reaction chamber and the central chamber, the heat exchanger having a smaller thickness than the reaction chamber; and
an expansion region disposed at an outlet of the heat exchanger at a bottom portion of the auxiliary reformer and configured to create a uniform distribution of gas at an inlet of the reaction chamber, and wherein a thickness of the heat exchanger increases in the expansion region.